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| ChemSep v6.2 Released |
August 2008 |
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Version 6.2
includes a new feed-stage model, an improved relative volatility model, convergence methods,
and solve options. The GUI now shows the physical properties for all streams (including feeds,
products, and those inside the column). A new analysis tool can quickly plot binary physical
property diagrams and allow comparisons with data, to enable correct model selection.
Usability of the GUI has increased with a configurable toolbar, plots can be copied and pasted
as EMF files, and sep files are automatically backed up. A complete new (physical) property data
manager has been added with many property estimation methods and a web search for adding new compounds.
It can plot temperature dependent properties and allows comparison with experimental data (loaded from,
for example, DIPPR or other databanks) for ensuring accurate simulation results.
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| ChemSep v6.1 Released |
March 2008 |
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The new version of ChemSep LITE has been released. New features include physical properties,
a more robust column solver, fully configurable toolbar and short-cut keys, and logging for all
property calculations. For the CAPE-OPEN column simulator we added energy ports, user parameters,
and column text reports. This new LITE version is incorporated in the new version of the
COCO Simulator (v1.10). A new chapter was added to the
ChemSep book on CAPE-OPEN and Flowsheeting that
covers the new features and illustrates the use of the ChemSep column simulator in flowsheets.
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| ChemSep LITE Extended |
August 2007 |
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Due to the popularity of ChemSep LITE simulator we have extended the number of compounds that can be used
from five to ten and the number of equilibrium stages from 50 to 150. These extended limits will enable the
simulation of industrial processes. Also enhanced are the binary VLE Analysis and tray rating and costing
of equilibrium column simulations (where the results can be directly loaded into the tools of the industrial
vendors).
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| Benchmarking MTC models |
May 2007 |
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At the
EFCE Distillation and Absorption Working Party
meeting at the TU Delft a
benchmarking overview
was presented for mass transfer models of structured packings. It was shown that for the cyclohexane/normal-heptane
test mixture the HETP needs to be computed as an average by integrating over the packed bed when comparing the
performances of MTC models. For this test mixture, which replaced the benzene/toluene, the relative volatility
can change by more than ten percent! Physical properties are also not constant and the HETP varies differently
at different pressures. Yet this mixture is most commonly used for testing packings in distillation service.
Therefore, we started the construction of an online database for distillation test data available from the open
literature to determine the models best suited for predicting the performance of modern packings and trays.
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| CAPE-OPEN Overhead Determined |
November 2006 |
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At the national AIChE Meeting in San Francisco we
presented
some tangible numbers on the computational overhead involved with CapeOpen process calculations
with ChemSep+COCO and ChemSep+AspenPlus. The ratio between running flash and column
simulations with or without CapeOpen is a factor of about 2.5.
Interesting is that this average is not influenced by the number of compounds in the
simulations, the tests were performed with 20-200 pseudo compounds in a crude oil mixture.
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| ChemSep Version 6 |
October 2006 |
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In October we launch the new version of ChemSep, version 6, which includes many
new features, such as Residue Curve Maps,
ternary VLE diagrams, Parametric Study mode, constant relative volatility and Universal Mixing
Rule (Voutsas et al.) thermodynamic models, as well as physical property calculations.
Visit our site in October to test-drive these with ChemSep-LITE.
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| ChemSep in Motion |
March 10 2006 |
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At the recent CAPE-OPEN meeting in
Cannes, France, progress was
reported
on the interoperability of the ChemSep CAPE-OPEN Unit Operation with commercial flowsheeting packages
Aspen Plus (AspenTech), PRO/II (SIMSCI), and Aspen HYSYS (AspenTech), as well as with the flowsheeting
package COCO which was designed completely from CAPE-OPEN
principles. A simple C3/C4 splitter with a purity specification is used as a test case. Tested was the
capability to run the ChemSep column unit operation in the flowsheeter, whether it was possible to
obtain thermodynamics and pure component data from the flowsheeter, and whether the flowsheeter allowed
changing the ports of the unit (that is feeds/products of the column). All column operations give very
similar numerical answers for the C3/C4 splitter test case. ChemSep LITE is now CAPE-OPEN and available
for free. Interoperability of ChemSep-LITE and COCO was
illustrated by simulation of a complete three column cryogenic Air Separation Unit with crude Argon
production, using exclusively CAPE-OPEN unit operations and thermodynamics.
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| ChemSep-LITE is now CAPE-OPEN |
December 2005 |
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The new LITE version includes our CAPE-OPEN ChemSep User Operation model that allows you to include
a ChemSep column simulation inside flowsheet simulators such as Aspen Plus
(www.aspentech.com)
or COCO (www.amsterchem.com) that have proper unit operation
support via the Cape-Open protocol. The CAPE-OPEN version was developed in collaboration with AmsterChem.
This new release also includes various bug-fixes and a new initialization routine that improves the
convergence of the column simulators.
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| ChemSep v5.1 Released |
August 2005 |
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This new release includes valuable additions such as the Pure Component Data manager which allows
you to add components to the database (also for LITE) and the parametric study analysis option enables
you to study the effect of varying operational or hardware parameters on product purities or column
dimensions. We also improved the automatic initialization method as well as the way we perform our
simulations. The LITE version is available on the downloads page (the CACHE version will be
available from September).
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| Chemsep CAPE-OPEN presented |
February 2005 |
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The CAPE-OPEN version of ChemSep was presented at the COLAN
meeting in Como, Italy
(presentation PDF and
example PDF).
Columns can be solved using the ChemSep nonequilibrium model inside flowsheets running
under HYSYS (TM) or ASPEN Plus (TM), both products of AspenTech.
The column simulator can use thermodynamic and physical properties as supplied by the flowsheeting
package or the properties as supplied by the ChemSep libraries.
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| ChemSep-LITE Free Download |
January 2005 |
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A free, "lite" version of the new windows version of ChemSep (v5.0) is now available for download.
The ChemSep-LITE version is limited in
the number of stages and components and only includes the equilibrium column model but many text book
examples can be solved with this lite version of ChemSep. Also total-reflux experiments can be simulated
with this version. The ChemSep-LITE is free for all use (also commercial) and comes without any
guarantee or support. You use it at your own risk.
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Copyright © Sun Aug 10 00:30:19 2008 ChemSep
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